|Publication number||US7179287 B2|
|Application number||US 10/260,007|
|Publication date||Feb 20, 2007|
|Filing date||Aug 13, 2002|
|Priority date||Nov 22, 1999|
|Also published as||US6416995, US6432712, US20030219417|
|Publication number||10260007, 260007, US 7179287 B2, US 7179287B2, US-B2-7179287, US7179287 B2, US7179287B2|
|Inventors||Lloyd Wolfinbarger, Jr.|
|Original Assignee||Bioscience Consultants|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (11), Non-Patent Citations (8), Referenced by (23), Classifications (24), Legal Events (2)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This application is a continuation of application Ser. No. 09/595,717, filed Jun. 6, 2000, now U.S. Pat. No. 6,432,712.
The invention provides a device and process for decellularizing, and/or devitalizing, tissue grafts, and/or recellularizing, essentially acellular or devitalized tissue grafts, including for example essentially acellular or devitalized vascular tissue grafts, where the graft is derived from a human or animal sources, or is as constructed using any number of tissue engineering methodologies.
Vascular grafts include a wide variety of natural and synthetic tubular structures that may or may not contain valves. Valves in these tubular structures are usually intended to direct the flow of blood (or other nutrient materials) in one direction by preventing the backward flow of this (these) liquid solution(s). Examples of valved tubular structures include aortic, pulmonary, and mitral valves present in the hearts of most vertebrate animals and veins used to return blood flow from the periphery of the body to the heart for recirculation.
Vascular grafts constructed of synthetic materials include devices constructed from man-made polymers, notably Dacron and Teflon in both knitted and woven configurations such as those marketed by W. L. Gore, Inc. and Impra, Inc. where various forms of polytetrafluoroethylene (PTFE) are molded into a wide array of tubule structures (see for example U.S. Pat. Nos. 4,313,231; 4,927,676; and 4,655,769.
Natural vascular grafts, taken in the context of the invention, include valved and non-valved tubular structures obtained by methodologies broadly classified under the term “tissue engineering”. Notably, tissue engineered blood vessels such as described in U.S. Pat. Nos. 4,539,716, 4,546,500, 4,835,102, and blood vessels derived from animal or human donors such as described in U.S. Pat. Nos. 4,776,853, 5,558,875, 5,855,617, 5,843,181, 5,843,180, and a pending patent application entitled “A Process for Decellularizing Soft-Tissue Engineered Medical Implants” (patent application Ser. No. 09/528,371 incorporated herein in its entirety). The present invention involves vascular grafts derived using a novel process associated with tissue engineering as well as a novel bioreactor device for use in the process.
Tissue engineered natural vascular grafts, hereinafter vascular grafts, can be manufactured by processing of natural vascular grafts (including for example, veins, arteries, and heart valves.) with the objective of removing the cellular elements without damaging the matrix structure of that tissue—a “reductionist” approach. This approach is generally referred to as decellularization and is the subject of several patents, of which U.S. Pat. No. 4,801,299 by Brendel and Duhamel is considered as one of the earliest such patents, and pending patent applications as described above. Decellularization of tissues has been attempted by incubating tissues in the presence of detergents, both anionic and nonionic, with and without digestion of nucleic acids.
Tissue engineered natural vascular grafts have also been constructed using a “constructionist” approach. This approach involves the extraction of natural cellular and matrix components to obtain purified (or partially purified) fractions and then using these fractions to reconstruct a vascular graft from individual components. Alternatively, specific components of a vascular graft, for example collagen(s), can be obtained using recombinant DNA technologies and such highly purified and homogeneous materials used in the construction of natural vascular grafts via tissue engineering. Methods and materials for 3-dimensional cultures of mammalian cells are known in the art. See, U.S. Pat. No. 5,266,480. Typically, a scaffold is used in a bioreactor growth chamber to support a 3-dimensional culture. The scaffold can be made of any porous, tissue culture compatible material(s) into which cultured mammalian cells can enter and attach.
Both the reductionist and constructionist approaches are attempts to provide an acellular matrix that can be used directly as an acellular graft.
The invention provides a bioreactor approach to reseeding of vascular grafts, such as a decellularized aortic heart valve. The approach involves removal of the basement membrane by enzymatic digestion. This removal of basement membrane is followed by pressure-differential induced movement of fibroblastic cells in a solution into the matrix structure and reendothelialization by incorporation of endothelial cells into a collagenous/noncollagenous solution. This latter solution is compacted, as necessary, by “pressure” binding of this mixture onto the luminal surface to recreate a “basement membrane” containing endothelial cells. Cells are induced to resume metabolic activities following treatment with specific growth factors, for example fibroblast growth factor, or platelet aggregation under a pulsatile flow of nutrient solutions. The novel design of the bioreactor facilitates the processes described in the present invention.
According to one aspect of the present invention, a device and process is described for recellularizing and reendothelializing essentially acellular or devitalized tissue grafts including vascular grafts for use in replacement of defective tissues including for example defective heart valves and vascular conduits. The device is a bioreactor designed to facilitate selected steps in the processing such as recellularization and reendothelialization. The process includes several steps which may be conducted outside of the bioreactor and several steps which may be conducted inside of the bioreactor such that most of the invention is carried out in a closed processing system that will dramatically restrict contamination by microbiological and chemical/biological elements. The process comprises the following steps:
Preferred embodiments of the invention are shown in the drawings, wherein:
As used herein, “recellularization” means the repopulation of the matrix volume of a tissue engineered or devitalized tissue or decellularized-acellular matrix structure with a viable cell population that is either the desired cell phenotype and/or genotype or that which can be caused to differentiate into the desired cell phenotype and/or genotype.
As used herein, “reendothelialization means the repopulation of the flow surface of a tissue engineered or devitalized tissue or decellularized-acellular matrix structure with a viable endothelial cell population that is either phenotypically and/or genotypically an endothelial cell at the time of repopulation or that which can be caused to differentiate into the desired cell phenotype and/or genotype.
As used herein, “decellularization” means the removal of cells and cell remnants from a tissue matrix structure using liquid solution processing.
As used herein, “devitalized tissue” means a tissue having as it's major components collagens and elastin in the form of extracellular matrix from which has been removed cellular membranes, nucleic acids, and lipids, but retaining large molecular weight cytoplasmic proteins. These residual high molecular weight cytoplasmic proteins promote recellularization.
As used herein, “cell to cell communication” means the chemical and/or physical signaling between one or more cells and/or cell populations such that a given cell or cell population is stimulated to function in a manner necessary to the role of that cell in maintaining tissue function. This cell to cell communication can occur by paracrine types of signaling using large and small molecular weight factors and is generally restricted to within the tissue comprising the functional entity being observed or studied.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one skilled in the art of tissue processing and cell culturing techniques. Although materials and methods similar or equivalent to those described herein can be used in the practice or testing of the invention, the preferred methods and materials are described below. All publications, patent applications, patents and other references mentioned herein are incorporated by reference. In addition, the materials, methods, and examples are illustrative only and not intended to be limiting.
The bioreactor used in this invention is intended to be used as a closed system to restrict contamination of the vascular grafts material(s) being processed. One of the preferred embodiments of the bioreactor is illustrated in
The Process of recellularization and reendothelialization of a vascular graft, for example an aortic heart valve as described herein, can be described in general terms. The vascular graft is procured from a human or animal source and transported to the processing facility in a hypotonic solution, in a sterile bag, on wet ice. Once at the processing facility the tissue would be trimmed of excess muscle and fat, the proximal and distal ends cut smoothly perpendicular to the long axis of the tissue and/or optionally attaching to sewing rings, and mounted into the tissue holding O-ring constraints on the inlet (1) and outlet (2) end plates (as illustrated in
Decelluiarization.: If the tissue has not already been decellularized, or was not acellular following construction, the inflatable piston is caused to enter into the luminal volume of the tissue and inflated to approximately fill the luminal volume. A HEPES buffered (pH 6.0 to 7.5) hypotonic solution of non-ionic detergent(s), for example polyoxyethylene alcohol sold under the trademark BRIJ-35™ at 0.2 to 1.0 mM, preferably containing the commercially available recombinant endonuclease sold under the trademark BENZONASE™ by EM Industries, or other suitable enzyme preparations of DNase and RNase, is pumped into the luminal space of the graft through the inlet port of the inlet end plate and into the volume between the adventitial side of the graft and the jacket through the inlet port of the jacket. These fluids are allowed to exit the bioreactor via the outlet port in the jacket and the outlet port of the outlet end plate, returning to the peristaltic pump (9) for recirculation back into the bioreactor. In-line filters can optionally be used to remove particulate materials from the circulating solution, and this recirculation of decellularization solution is allowed to proceed for between three (3) and twelve (12) hours at temperatures between 20° C. and 37° C. Decellularization can be monitored at 260 nm for degradation products of the nucleic acids present in the cells being solubilized and degradation of cellular macromolecules. Ideally, the flow rates of decellularization solutions will be maintained such that slight positive pressure exists in the luminal volume of the tissue being decellularized.
Washing: When decellularization has been completed, the decellularization solution is washed from the bioreactor, tissue, and tubing by switching processing solutions to preferably ultrapure water, however various buffered salt solutions, made hypotonic or hypertonic, may be substituted as required to remove residual cellular elements, and diverting the effluent solution flow to waste. Washing volumes need to involve volumes in excess of 10 volume changes of the bioreactor volume.
Treatment: The treatment phase of the process is optional, but desirable. The treatment phase of the process involves recirculation flow of aqueous solutions into, through and around the tissue in the bioreactor. This recirculation flow involves flow of solutions through both the luminal and adventitial (i.e. volume between the adventitial surface of the tissue and the jacket) volumes. Treatment solutions, for purposes of this specific process include low ionic strength HEPES (or similar Good buffer) buffered (pH 6.5–7.4) aqueous solutions of fibroblast growth factor (0.1 nM to 0.1 μM), suramin (0.001% to 1.0% by weight), sodium dodecylsulfate (0.001% to 1.0% by weight), bone morphogenetic protein(s) 1, 2, 6, and 7 (0.01 nM to 0.1 μM), aggrecan (0.0001% to 0.01% by weight), hyaluronins (0.0001% to 0.1% by weight), interleukin 6 (0.001 nM to 0.1 nM), glutathione ethylester (or glutathionine), and/or transferin. Recirculation volumes may be minimized by inserting and inflating the inflatable piston in the luminal volume of the graft.
Washing: When treatment has been completed, the treatment solution(s) is (are) washed from the bioreactor, tissue, and tubing by switching processing solutions to preferably ultrapure water, optionally supplemented with glutathione ethylester, however various buffered salt solutions or alcohol solutions may be substituted as required to remove residual cellular elements and treatment agents, and diverting the effluent solution flow to waste. Washing volumes need to involve volumes in excess of 10 volume changes of the bioreactor volume.
Basement Membrane Removal/Perforation: With the inflatable piston in the inflated position, buffered solutions of proteolytic and/or hydrolytic enzymes can be injected through the sample inject (10) and pumped into the luminal volume of the tissue via the inlet port of the inlet end plate. During this process, the outlet port of the outlet end plate needs to be opened. When the volume present in the luminal volume of the tissue has been replaced by the proteolytic solution, the inlet port and outlet ports of the inlet and outlet end plates can be closed. For this step of the process, both the inlet and outlet ports of the jacket remain in the closed position. The proteolytic enzymes used in this step of the process include trypsin, chymotrypsin, elastase, collagenase, dispase, ficin, papain, and/or alkaline protease. The hydrolytic enzymes used in this step of the process include hyaluronidase, glucuronidase, and/or neuraminidase. The enzymes may be free in solution or attached to microscopic beads, such that hydrolysis of basis membrane will occur only where these microscopic beads, to which hydrolytic enzymes are tightly attached, come in physical contact with the basement membrane. See for example immobilized papain, pepsin, trypsin as attached to cross-linked 6%/4% beaded agarose and available from Pierce Chemical Company (product numbers 20341ZZ, 20343ZZ and 20233ZZ, respectively). Alternatively, specific bacterial species which produce and secrete specific hydrolytic enzymes, for example Clostridium histolyticum for collagenase, Bacteroides gingivalis, Fusobacterium nucleatum, Actinobacillus actinomycetemcomitans, and/or mammalian cells such as U937 monoblastoid cells, and/or an oral flagellate such as Trichomonas tenax, can be used instead of the microscopic beads (to which hydrolytic enzymes are attached) to digest holes in the basement membrane. This step in the process is intended to be of only sufficient time to permit digestion of a significant portion of the basement membrane (that membrane to which the endothelial cells attach in a native tissue) to allow penetration of the fibroblastic cell population into the matrix structure. The time intervals, enzymes, enzyme concentrations, and buffer conditions will be dictated by the type of graft being treated and the condition of the basement membrane of the tissue at the time of treatment. For example, for an aortic valve denuded of endothelial cells during the initial cold transport in hypotonic solutions, an appropriate enzyme concentration and time might include, but not be limited to, the enzyme collagenase at 0.01 IU/ml to 1.0 IU/ml for periods of time between 30 to 180 minutes. Times that can be expected to achieve the desired digestion of basement membrane in a typical aortic heart valve. For aortic valves retaining a significant endothelial cell layer, dispase (0.01 IU/ml to 0.5 IU/ml) may need to be added to the collagenase solution to help remove the endothelial cells permitting access of the collagenase to the basement membrane. Use of trypsin, chymotrypsin, elastase, ficin, papain, and/or alkaline protease can be used to enhance basement membrane digestion, however they can also be expected to degrade the underlying tissue matrix if incubation times are greater than 30 to 60 minutes. Incubation temperatures should be between 20° C. and 37° C. By regulating the size(s) of the microscopic beads, or bacterial species, it should be possible to not only control the size(s) of the holes created in the basement membrane, but to control the number of holes per unit surface area of the basement membrane by controlling the density of the microscopic beads (bacteria) used in the treatment solution.
Washing: It is essential that the proteolytic and hydrolytic digestion of the basement membrane be terminated quickly and efficiently. Towards this end, washing of the tissue to terminate removal of the basement membrane should be accomplished at reduced temperatures, for example 0° C. to 5° C., with rapid flow of buffered (pH 5.0 to 6.0) water solutions through both the luminal and adventitial volumes of the bioreactor. Flow of these washing solutions should be directed to waste. Wash volumes should be in excess of 20 bioreactor volumes over a time interval of 30 to 180 minutes.
Fibroblast Cell Seeding: Fibroblast cell seeding through the sample inject (10) (
Approach number one: When the inflatable piston is present in the luminal volume of the graft, fibroblast cells (obtained from either primary tissue digests of the intended recipient of the graft (autograft cells) or from fibroblastic cells maintained in tissue culture (allograft cells)) will be pumped into the luminal volume of the graft via the inlet port of the inlet end plate. During the initial stages of delivery of the cells into this luminal volume, the outlet port of the outlet end plate will be open and the inlet and outlet ports of the jacket will be closed. The fibroblast cells will be at total viable cell numbers between 1×106 and 1×108 cells/tissue to be recellularized. The total number of cells to be infused into the matrix of a specific tissue will approximate 1000 to 10,000 cells/mm3 of tissue matrix. Once the cells have been delivered into the luminal volume of the tissue, the outlet port of the outlet end plate can be closed and the outlet port of the jacket opened (with flow directed to waste). The flow rate on the peristaltic pump can be reduced to achieve a minimal positive pressure in the luminal volume of the tissue. Solution being pumped is switched from a cell suspension to a nutrient and growth factor-rich tissue culture medium supplemented with glutathione ethylester (or similar antioxidant) and/or similar anti-apoptotic agents such as IGF-1 or ZVAD-fmk (a caspase inhibitor), but not supplemented with serum. Flow of this nutrient solution is maintained for between 3 to 12 hours, or until cells can be detected in the outflow solution from the bioreactor, at 37° C. After about 12 hours, flow of nutrient is directed out of the luminal volume of the tissue via the outlet port of the outlet end plate to waste.
Approach number two: When the inflatable piston is not present in the luminal volume of the graft, fibroblast cells (obtained from either primary tissue digests of the intended recipient of the graft (autograft cells) or from fibroblastic cells maintained in tissue culture (allograft cells)) can be added via the sample inject (10) (
Reendothelialization of the Tissue: Following removal of the fibroblastic cell population from the luminal volume of the graft, endothelial cells are mixed into a viscous, collagenous/non-collagenous, solution at total cell numbers calculated as necessary to cover the luminal surface of the graft being reendothelialized. Such total cell numbers may be calculated by anyone skilled in the art and knowing the surface area typically covered by an endothelial cell in a native vascular graft. The collagenous/noncollagenous solution will include antioxidants such as glutathione ethylester in nutrient medium and collagen primarily of type IV, derived by extraction of tissues or as a recombinant product, however other collagen types (for example, types I, II, V, VII and X) may be included as desired. The concentration of collagen can range between about 0.1% and 2% by weight. The endothelial cells may be derived as primary cultures from the intended recipient of the tissue graft (an autograft approach) or from endothelial cell cultures derived from cell banks (an allograft approach) which may or may not have been genetically manipulated to reduce immunogenicity or improve paracrine functions. In that endothelial cells express MHC antigens, an allograft approach to seeding of enthothelial cells would not be expected to be retained on the luminal surface of a reendothelialized graft for extended periods of time post transplantation.
Endothelial cells present in a collagenous/noncollagenous solution are injected into the system via the sample inject (10) (
The recellularized and reendothelialized tissue should be incubated at 37° C. for between 12 and 24 hours with a slow flow of nutrient and growth factor enriched HEPES buffered tissue culture medium supplemented with glutathione ethylester (or similar antioxidant), anti-apopotic agents such as, for example, IGF-1 and/or ZVAD-fmk (a caspase inactivator), fetal calf serum (or similar serum substitute if use of a serum-free medium is desired) and selenium/transferin as known to anyone skilled in the art of tissue culture additives. Flow rates can be determined by one skilled in the art of monitoring eluent medium for glucose, lactose, ammonia, etc., such that metabolic states of the cells can be determined and flow rates either increased or decreased according to nutrient depletion or waste product accumulation.
Graft Conditioning: Prior to transplantation, it may be desirable to precondition the graft by subjecting it to high pressure pulsatile flow of nutrient and growth factor enriched HEPES buffered tissue culture medium, at 37° C., supplemented glutathione ethylester (or similar antioxidant) and anti-apoptotic agents, for example IGF-1 and/or ZVAD-fmk (a caspase inactivator), with fetal calf serum (or similar serum substitute if use of a serum-free medium is desired) and selenium/transferin. The pressure and pulsatile flow patterns should be adjusted to simulate those pressures and pulsatile flow patterns to be found in the site in which the graft is to be implanted. The outlet port of the jacket should be open with flow of solution contained in the space between the tissue graft and the jacket directed to a pulse-dampening device to control the application of stress, and strain, to the graft. During this preconditioning, eluent solution should be monitored for fragments of collagen/endothelial cells. These will appear as particulate materials in the outflow side of the graft. Preconditioning times will vary with tissue graft type and desired alignment and orientation of the endothelial cells covering the luminal surface of the graft. Preconditioning is primarily directed at causing release of any collagen/endothelial cell fragments that will be release and to stimulating cell to cell interactions essential to long-term function and maintenance of a viable cell population in the tissue graft.
Cell Selection: Recellularization and reendothelialization of an acellular vascular graft can reasonably be expected to occur under the conditions described. However, it is important that the appropriate type of fibroblastic and endothelial cell population be selected for the recellularization/reendothelialization events. All cells, with the exception of reproductive cells such as eggs and sperm, are omnipotent, i.e. contain the same complement of genes and genetic material. However, some cells are more differentiated towards a given phenotype than other cells and there exists within fibroblastic cell populations in a body, fibroblastic cells with differing degrees of differentiation towards a specific phenotype. For example, there exist fibroblastic cells designated as myofibroblasts, based on tissue of origin, and these myofibroblasts may originate from aortic conduit tissue, myocardium, or similar contractile tissues. In that proper growth and differentiation factor mediated cell stimulation can be used to direct, or redirect, cell growth and differentiation, origin of a fibroblastic cell population to be used in recellularization of a cardiovascular tissue is less important than preventing triggering of a programmed cell death process commonly referred to as “apoptosis”. Morphologically, apoptosis is characterized by chromatic condensation, cell shrinkage, and membrane blebbing. Within the cell, various proteases and endonucleases are activated leading to degradation of protein and nucleic acids.
This is in contrast to the other mode of cell death, necrosis, which is uncontrolled in nature and is characterized by swelling and lysis of the cell. Oxidative stress is potentially a common signaling mechanism among diverse inducers of apoptosis and thus the inclusion of antioxidants or other agents such as IGF-1 and/or ZVAD-fmk (a caspase inactivator) in the processing and nutrient culture medium solutions described in this invention represents an important element of recellularization/reendothelialization designed to restrict programmed cell death in these tissues post-transplantation. Glutathione ethylester is a strong antioxidant that is freely permeable into cells. Although not claimed in this invention, it is theoretically possible to genetically manipulate cells used in repopulation of cardiovascular tissues by enhancing activity of genes acting as promoters (e.g. bax, Fas, and p 53) and effectors (ICE-like proteases) or inhibitors (e.g. bcl-2, bcr-abl) of the process. Bcr-abl can be an activated form of a gene that is antiapoptotic.
Thus, although the present invention is not directed towards use of specific fibroblastic or endothelial cells derived from specific tissues, it is an important aspect of the present invention to use metabolically and reproductively viable cell populations and to include in the various nutrient and processing solutions, additives which enrich the metabolic functions of these cells and which serve to restrict induction of the process of apoptosis until the cell populations can be properly oriented and stimulated, both mechanically and chemically, to resume proper cell to cell communication essential to long-term viability and function. Initial stimulation of the endothelial cells used to construct a new basement membrane or fill the holes in the basement membrane formed from the microscopic bead containing hydrolytic enzymes can occur via addition of fibroblast growth factor into the nutrient medium. In addition, however, platelets from the intended recipient, or donor-derived platelets, can be used to treat the newly constructed basement membrane. Addition of platelets to the bioreactor following inflatable piston compression of the collagenous/noncollagenous/endothelial cells construct will result in platelet aggregation and activation by the “rough” protein structure. This platelet aggregation and activation will serve a similar purpose as addition of fibroblast growth factor to the nutrient medium, or preaddition to the construct, and will localize delivery of essential growth and differentiation factors at the site on the new basement membrane where it is desired to have a smooth layer of overlapping and function endothelial cells.
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|U.S. Classification||623/1.41, 435/395, 435/325, 623/1.1, 435/174, 424/422|
|International Classification||A61F2/06, C12N11/00, A61L27/38, C12N5/06, A61F13/00|
|Cooperative Classification||Y10S623/921, Y10S623/916, C12M29/12, A61L2430/20, A61L27/507, A61L27/3895, C12M25/14, C12M21/08, C12M29/14, A61F2/062, A61L27/38|
|European Classification||A61F2/06B, A61L27/38|
|Aug 5, 2010||FPAY||Fee payment|
Year of fee payment: 4
|Aug 20, 2014||FPAY||Fee payment|
Year of fee payment: 8